glycerol dehydrogenase

Author(s):  
C.‐H. Wong
1968 ◽  
Vol 46 (9) ◽  
pp. 1107-1114 ◽  
Author(s):  
Jean Himms-Hagen

The endogenous rate of glycerol production in rabbits was measured by several techniques: constant infusion of 1,3-14C-glycerol or 2-3H-glycerol or unlabeled glycerol; single injection of 1,3-14C-glycerol or 2-3H-glycerol or unlabeled glycerol. The rate was 5.5–11.6 μmoles/kg per minute (9 rabbits). The mean fractional turnover rate was 0.0585 ± 0.0052. During infusion of noradrenaline together with 3H-glycerol, the fractional turnover rate was no different from that in the absence of noradrenaline. The maximum utilization rate of glycerol was 28.1 ± 1.40 μmoles/kg per minute. The glycerol space was 58.1% of body weight. The relationship of glycerol concentration to rate of glycerol utilization in the intact rabbit suggests the existence of an enzyme with a KM for glycerol of 0.33 × 10−3 M; the glycerol kinase of rabbit liver was found to have a KM for glycerol of 0.29 × 10−3 M. This enzyme could account for the disappearance of glycerol in the intact animal except that its Vmax is only 4% of that expected. Possible reasons for this are discussed. A glycerol dehydrogenase with a Vmax similar to that of the glycerol kinase also exists in rabbit liver; its KM for glycerol is so high (0.5 M) that it is unlikely to play a significant role in glycerol metabolism in the normal rabbit.


2009 ◽  
Vol 25 (5) ◽  
pp. 1372-1378 ◽  
Author(s):  
Tsuyoshi Mouri ◽  
Takeshi Shimizu ◽  
Noriho Kamiya ◽  
Masahiro Goto ◽  
Hirofumi Ichinose

Author(s):  
Paul Musille ◽  
Eric Ortlund

The 1.90 Å resolution X-ray crystal structure of glycerol dehydrogenase derived from contaminating bacteria present during routineEscherichia coliprotein expression is presented. This off-target enzyme showed intrinsic affinity for Ni2+-Sepharose, migrated at the expected molecular mass for the target protein during gel filtration and was crystallized before it was realised that contamination had occurred. In this study, it is shown that liquid chromatography coupled to tandem mass spectrometry (LC-MS/MS) can efficiently identify the protein composition of crystals in a crystallization experiment as part of a structure-determination pipeline for an unknown protein. The high-resolution X-ray data enabled sequencing directly from the electron-density maps, allowing the source of contamination to be placed within theSerratiagenus. Incorporating additional protein-identity checks, such as tandem LC-MS/MS, earlier in the protein expression, purification and crystallization workflow may have prevented the unintentional structure determination of this metabolic enzyme, which represents the first enterobacterial glycerol dehydrogenase reported to date.


1982 ◽  
Vol 24 (4) ◽  
pp. 971-975 ◽  
Author(s):  
A. K. Chen ◽  
J. A. Starzmann ◽  
C. C. Liu

2017 ◽  
Vol 92 ◽  
pp. 417-424 ◽  
Author(s):  
Aishwarya Mahadevan ◽  
Sandun Fernando

1992 ◽  
Vol 22 (4) ◽  
pp. 293-296 ◽  
Author(s):  
Heather M. Sealy-Lewis ◽  
Valerie Fairhurst

Author(s):  
Sadat M. R. Khattab ◽  
Takashi Watanabe

Glycerol is an eco-friendly solvent that enhances plant biomass decomposition via glycerolysis in many pretreatment methods. Nonetheless, inefficient conversion of glycerol to ethanol by natural Saccharomyces cerevisiae limits its use in these processes. Here, we have developed an efficient glycerol-converting yeast strain by genetically modifying the oxidation of cytosolic nicotinamide adenine dinucleotide (NADH) by an O 2 -dependent dynamic shuttle and abolishing both glycerol phosphorylation and biosynthesis in S. cerevisiae D452-2 strain, as well as vigorous expression of whole genes in the DHA-pathway ( Candid utilis glycerol facilitator, Ogataea polymorpha glycerol dehydrogenase, endogenous dihydroxyacetone kinase, and triosephosphate isomerase). The engineered strain showed conversion efficiencies (CE) up to 0.49 g ethanol/g glycerol (98% of theoretical CE), with production rate >1 g/L −1 h −1 when glycerol was supplemented in a single fed-batch fermentation in a rich medium. Furthermore, the engineered strain converted a mixture of glycerol and glucose into bioethanol (>86 g/L) with 92.8% CE. To the best of our knowledge, this is the highest reported titer of bioethanol produced from glycerol and glucose. Notably, we developed a glycerol-utilizing transformant from parent strain, which cannot utilize glycerol as a sole carbon source. The developed strain converted glycerol to ethanol with a productivity of 0.44 g/L −1 h −1 on minimal medium under semi-aerobic conditions. Our findings will promote the utilization of glycerol in eco-friendly biorefineries and integrate bioethanol and plant-oil industries. IMPORTANCE With the development of efficient lignocellulosic biorefineries, glycerol has attracted attention as an eco-friendly biomass-derived solvent that can enhance the dissociation of lignin and cell wall polysaccharides during the pretreatment process. Co-conversion of glycerol with the sugars released from biomass after glycerolysis increases the resources for ethanol production and lowers the burden of component separation. However, low conversion efficiency from glycerol and sugars limits the industrial application of this process. Therefore, the generation of an efficient glycerol-fermenting yeast will promote the applicability of integrated biorefineries. Hence, metabolic flux control in yeast grown on glycerol will lead to the generation of cell factories that produce chemicals, which will boost biodiesel and bioethanol industries. Additionally, the use of glycerol-fermenting yeast will reduce global warming and generation of agricultural waste, leading to the establishment of a sustainable society.


1995 ◽  
pp. 592-596
Author(s):  
Dietmar Schomburg ◽  
Dörte Stephan

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